WO2013160562A1 - Method for finely feeding granular solids into liquid - Google Patents

Method for finely feeding granular solids into liquid Download PDF

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Publication number
WO2013160562A1
WO2013160562A1 PCT/FI2013/050469 FI2013050469W WO2013160562A1 WO 2013160562 A1 WO2013160562 A1 WO 2013160562A1 FI 2013050469 W FI2013050469 W FI 2013050469W WO 2013160562 A1 WO2013160562 A1 WO 2013160562A1
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WO
WIPO (PCT)
Prior art keywords
liquid
granular
mixing space
space
solid matter
Prior art date
Application number
PCT/FI2013/050469
Other languages
French (fr)
Inventor
Tapio Ritvanen
Original Assignee
S.T. Ritvanen Oy
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by S.T. Ritvanen Oy filed Critical S.T. Ritvanen Oy
Priority to US14/395,340 priority Critical patent/US10010836B2/en
Priority to EP13782117.9A priority patent/EP2841189A4/en
Publication of WO2013160562A1 publication Critical patent/WO2013160562A1/en

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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/80—Falling particle mixers, e.g. with repeated agitation along a vertical axis
    • B01F25/83—Falling particle mixers, e.g. with repeated agitation along a vertical axis with receptacles provided with fixed guiding elements therein, e.g. baffles; Cross-mixers comprising crossing channels for guiding the falling particles
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/10—Mixing by creating a vortex flow, e.g. by tangential introduction of flow components
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/50—Mixing liquids with solids
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/50—Mixing liquids with solids
    • B01F23/51—Methods thereof
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/20—Jet mixers, i.e. mixers using high-speed fluid streams
    • B01F25/21—Jet mixers, i.e. mixers using high-speed fluid streams with submerged injectors, e.g. nozzles, for injecting high-pressure jets into a large volume or into mixing chambers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers
    • B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/71—Feed mechanisms
    • B01F35/717—Feed mechanisms characterised by the means for feeding the components to the mixer
    • B01F35/7173—Feed mechanisms characterised by the means for feeding the components to the mixer using gravity, e.g. from a hopper
    • B01F35/71731—Feed mechanisms characterised by the means for feeding the components to the mixer using gravity, e.g. from a hopper using a hopper
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/50—Mixing liquids with solids
    • B01F23/56—Mixing liquids with solids by introducing solids in liquids, e.g. dispersing or dissolving

Definitions

  • the invention relates to a method for finely feeding granular solids into a liquid, in which method granular solids and a liquid are fed into a mixing space and mixed together, and a mixture of small solid particles and liquid is discharged from the mixing space.
  • Fine-grained feeding of solids into a liquid is needed in a variety of processes. For example, these include processes, in which different ingredients are separated from a liquid, processes, in which continuously circulating cleaning waters and/or cleaning liquids are regenerated during circulation and processes, in which various catalysts are added and/or colours are controlled.
  • the object of the invention is to provide a method by which the prior-art drawbacks can be eliminated. This is achieved by a method according to the invention.
  • the method of the invention is characterized in that the granular solid matter in the mixing space is subjected to a liquid flow in such a manner that the liquid flow is driven into a mass consisting of the granular solids and the granular solids are brought to roll controllably in a controlled rolling space locating in the mixing space, whereby the grains of the granular solids abrase one another while rolling and tiny particles detaching in abrasion are carried away from the mixing space along with the liquid and large grain particles continue rolling in the controlled rolling space.
  • An advantage of the invention is, above all, its simplicity. Another advantage of the invention is that the end result is of very high quality, in other words, the quality of fine-grained feeding of solids in comparison with the quality achievable by the prior art is considerably higher. A further advantage of the invention is that the operating costs of the method according to the in- vention are very low, for instance, need for maintenance is insignificant in comparison with the prior art.
  • Figure 1 is a general view of an embodiment utilizing the method of the invention.
  • Figure 2 is a general view of a flow situation, without walls, in the embodiment of Figure 1 .
  • FIG. 1 is a general view of an embodiment applying the method of the invention.
  • Reference numeral 1 denotes a container, in which is arranged a mixing space 2 in which granular solid matter 3 and a liquid to be mixed are fed.
  • the mixing space is formed by means of a partition wall 4 in the example of Figure 1 .
  • the liquid is circulated through the mixing space 2 in the container 1 by feeding the liquid into the mixing space through an inlet connection 5 and it is discharged from the mixing space through an outlet connection 6.
  • the partition wall 4 is arranged such that the granular solids 3 are able to run via a slot arranged between the partition wall 4 and a wall of the container 1 into the area 7 in the lower part of the mixing space as the process proceeds.
  • Figure 2 illustrates the same matter as Figure 1 , with the difference that Figure 2 does not show the container and the partition wall, but only the liquid and the granular solids.
  • the liquid into which the solids are to be fed is arranged to circulate in such a manner that the granular solids will be made roll controllably as a granular mass in a specified rolling space in a phase of the liquid flow circulation, without that the grains would be carried into the actual flow circulation.
  • the solid grains roll in the controlled rolling space, they collide with one another and simultaneously get chafed, and consequently tiny particles detach therefrom, which tiny particles will be carried along with the actual flow circulation of the liquid, and larger grains will continue to roll in the rolling space.
  • the geometry of the rolling space for granular solids is defined by several details. For instance, a difference in the specific weight between the solid matter and the liquid affects whether it is possible to utilize gravity in preventing rolling grains from accessing the actual liquid flow circulation through the mixing space.
  • Figures 1 and 2 show a geometrical model, in which finegrained feed of granular solid matter into a liquid can be implemented by driving a liquid flow into the granular solid matter mass horizontally from the side.
  • a mixing space 2 via which the liquid is arranged to circulate through connections 5 and 6, is arranged inside a container 1 .
  • the liquid is arranged to flow horizontally via an inlet connection 5 so that the liquid flow is driven into a mass consisting of granular solids 3.
  • the flow is driven into the mass in such a way that the grains of the granular solid matter 3 start rolling by the effect of the liquid running via the inlet connection 5.
  • the rolling takes place in a controlled rolling space 8.
  • the mixing space 2 By arranging the mixing space 2 to be sufficiently large in relation to the rolling space 8 a situation is provided, in which the grains of the granular solid matter rolling in the mixing space 8 do not come into contact with any structure defining the mixing space 2, for instance, with a partition wall 2 and/or a wall of the container 1 . In that case the grinding process of the solid matter 3 does not wear any part of the apparatus.
  • the above involves two significant advantageous features. Firstly, the maintenance costs will reduce, and secondly, harmful particles originating from the structure of the apparatus will not end up in the liquid circulation.
  • the flow rate of the circulating liquid within this area will be so low that the grains of the granular solids move along with the liquid only for a while and then sink in order to soon restart moving along with the flow.
  • the motion of the grains of the granular solids in the rolling space is relatively slow, and consequently the grains abrase very slowly, and thus fine-grained abrasion particles will be carried little by little along with the circulating liquid.
  • FIG. 1 shows the same features as Figure 1 . However, Figure 2 reveals better the location of the granular solids, for instance, in the area 7, and also the essence of the rolling space 8.
  • the liquid flow is directed horizontally to the granular solid matter.
  • the granular solid matter is mostly heavier than the liquid.
  • the rolling of the granular solid matter in order to abrase it, is advantageously implemented by guiding the liquid circulation through the granular mass from below upward, whereby gravity makes the grains lifted by the circulation sink in the rolling and the liquid circulation lifts them up again.
  • This basic principle is applied also in the example of Figures 1 and 2, in which a horizontal liquid flow turns upwardly and the flow lifts grains upwardly and gravity, in turn, draws the grains down, as described above.
  • a flow is directed horizontally into the granular solid matter.
  • the circulating liquid may also be directed vertically, for instance, from above downward, close to the surface of the granular solids, whereby the liquid flow is driven vertically a short distance into the granular solid matter and turns then upwards bringing along grains that rise into a crater around a hole formed in the granular solid matter.
  • the obtained crater does not remain high, however, when a new hole is being bored from below into the granular solid matter, but the grains run back into the bored hole providing the desired rolling, i.e. the rolling space.
  • the direction in which the flow is directed into the granular solid matter may vary freely, in other words, the direction may be other than what is described above.
  • Figure 1 shows a cylindrical container, for instance. It is obvious that the container may be different from the cylindrical container shown in the figures, etc.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)
  • Treatment Of Sludge (AREA)

Abstract

A method for finely feeding granular solids into a liquid, in which method granu- lar solids (3) and a liquid are fed into a mixing space (2) and mixed together, and a mixture of small solid particles and liquid is discharged from the mixing space (2).The granular solid matter (3) in the mixing space is subjected to a liquid flow in such a manner the granular solids are brought to roll controllably in a controlled rolling space (8) locating in the mixing space (2), whereby the grains of the granular solids abrase one another while rolling and tiny particles detaching in abrasion are carried away from the mixing space (2) along with the liquid and large grain particles continue rolling in the controlled rolling space (8). (Figure 1)

Description

Method for finely feeding granular solids into liquid
[0001] The invention relates to a method for finely feeding granular solids into a liquid, in which method granular solids and a liquid are fed into a mixing space and mixed together, and a mixture of small solid particles and liquid is discharged from the mixing space.
[0002] Fine-grained feeding of solids into a liquid is needed in a variety of processes. For example, these include processes, in which different ingredients are separated from a liquid, processes, in which continuously circulating cleaning waters and/or cleaning liquids are regenerated during circulation and processes, in which various catalysts are added and/or colours are controlled.
[0003] In fields involving the above-mentioned processes there are developed various solutions which are to provide a high-quality fine-grained feed of solids into a liquid. The solutions disclosed in JP publication 2004338121 A1 , PCT publication WO 2009/048337 A1 , DE publication 1 174 744, EP publication 0 768 1 13 A1 and US publication 3 727 760 can be given as examples of the above-mentioned known solutions.
[0004] A drawback with the prior art has been the complexity and also the fact that the end result achieved by the technique concerned has not been the best possible.
[0005] The object of the invention is to provide a method by which the prior-art drawbacks can be eliminated. This is achieved by a method according to the invention. The method of the invention is characterized in that the granular solid matter in the mixing space is subjected to a liquid flow in such a manner that the liquid flow is driven into a mass consisting of the granular solids and the granular solids are brought to roll controllably in a controlled rolling space locating in the mixing space, whereby the grains of the granular solids abrase one another while rolling and tiny particles detaching in abrasion are carried away from the mixing space along with the liquid and large grain particles continue rolling in the controlled rolling space.
[0006] An advantage of the invention is, above all, its simplicity. Another advantage of the invention is that the end result is of very high quality, in other words, the quality of fine-grained feeding of solids in comparison with the quality achievable by the prior art is considerably higher. A further advantage of the invention is that the operating costs of the method according to the in- vention are very low, for instance, need for maintenance is insignificant in comparison with the prior art.
[0007] In the following, the invention will be explained in greater detail by means of an example described in the attached drawing, in which
Figure 1 is a general view of an embodiment utilizing the method of the invention, and
Figure 2 is a general view of a flow situation, without walls, in the embodiment of Figure 1 .
[0008] Figure 1 is a general view of an embodiment applying the method of the invention. Reference numeral 1 denotes a container, in which is arranged a mixing space 2 in which granular solid matter 3 and a liquid to be mixed are fed. The mixing space is formed by means of a partition wall 4 in the example of Figure 1 . The liquid is circulated through the mixing space 2 in the container 1 by feeding the liquid into the mixing space through an inlet connection 5 and it is discharged from the mixing space through an outlet connection 6. In the example of Figure 1 the partition wall 4 is arranged such that the granular solids 3 are able to run via a slot arranged between the partition wall 4 and a wall of the container 1 into the area 7 in the lower part of the mixing space as the process proceeds.
[0009] Figure 2 illustrates the same matter as Figure 1 , with the difference that Figure 2 does not show the container and the partition wall, but only the liquid and the granular solids.
[0010] In the method of the invention for finely feeding solids into a liquid the essential thing is that the liquid into which the solids are to be fed is arranged to circulate in such a manner that the granular solids will be made roll controllably as a granular mass in a specified rolling space in a phase of the liquid flow circulation, without that the grains would be carried into the actual flow circulation. When the solid grains roll in the controlled rolling space, they collide with one another and simultaneously get chafed, and consequently tiny particles detach therefrom, which tiny particles will be carried along with the actual flow circulation of the liquid, and larger grains will continue to roll in the rolling space.
[0011] The geometry of the rolling space for granular solids is defined by several details. For instance, a difference in the specific weight between the solid matter and the liquid affects whether it is possible to utilize gravity in preventing rolling grains from accessing the actual liquid flow circulation through the mixing space.
[0012] Figures 1 and 2 show a geometrical model, in which finegrained feed of granular solid matter into a liquid can be implemented by driving a liquid flow into the granular solid matter mass horizontally from the side.
[0013] As stated above, in the application of Figures 1 and 2, a mixing space 2, via which the liquid is arranged to circulate through connections 5 and 6, is arranged inside a container 1 . The liquid is arranged to flow horizontally via an inlet connection 5 so that the liquid flow is driven into a mass consisting of granular solids 3. In the example of Figures 1 and 2 the flow is driven into the mass in such a way that the grains of the granular solid matter 3 start rolling by the effect of the liquid running via the inlet connection 5. The rolling takes place in a controlled rolling space 8.
[0014] By arranging the mixing space 2 to be sufficiently large in relation to the rolling space 8 a situation is provided, in which the grains of the granular solid matter rolling in the mixing space 8 do not come into contact with any structure defining the mixing space 2, for instance, with a partition wall 2 and/or a wall of the container 1 . In that case the grinding process of the solid matter 3 does not wear any part of the apparatus. The above involves two significant advantageous features. Firstly, the maintenance costs will reduce, and secondly, harmful particles originating from the structure of the apparatus will not end up in the liquid circulation.
[0015] Because the cross sectional area of the mixing space 2 at the rolling space 8 is considerably larger than the cross sectional area of the inlet connection 5, the flow rate of the circulating liquid within this area will be so low that the grains of the granular solids move along with the liquid only for a while and then sink in order to soon restart moving along with the flow. The motion of the grains of the granular solids in the rolling space is relatively slow, and consequently the grains abrase very slowly, and thus fine-grained abrasion particles will be carried little by little along with the circulating liquid.
[0016] Slow abrasion of grains taking place in the rolling space 8 is replaced by a refill from a grain mass running from an area 7. A partition wall 4 retains a larger amount of granular solids in order for not producing an excessive counterpressure to the movement of the circulating liquid. [0017] Figure 2 shows the same features as Figure 1 . However, Figure 2 reveals better the location of the granular solids, for instance, in the area 7, and also the essence of the rolling space 8.
[0018] In the example of Figures 1 and 2 the liquid flow is directed horizontally to the granular solid matter. The granular solid matter is mostly heavier than the liquid. In that case the rolling of the granular solid matter, in order to abrase it, is advantageously implemented by guiding the liquid circulation through the granular mass from below upward, whereby gravity makes the grains lifted by the circulation sink in the rolling and the liquid circulation lifts them up again. This basic principle is applied also in the example of Figures 1 and 2, in which a horizontal liquid flow turns upwardly and the flow lifts grains upwardly and gravity, in turn, draws the grains down, as described above.
[0019] The smaller the difference in specific weights between the solid matter and the liquid, the more the liquid circulation rate is to be reduced in the rolling space 8, in order that the grains will not be carried along with the circulation, or vice versa. In that case it is advantageous to arrange in the liquid circulation a substantially expanding space, on the bottom of which is applied a desired amount of granular solids. An arrangement of this kind is shown in Figures 1 and 2.
[0020] As described above, in the example of Figures 1 and 2 a flow is directed horizontally into the granular solid matter. This is not the only possibility, however. The circulating liquid may also be directed vertically, for instance, from above downward, close to the surface of the granular solids, whereby the liquid flow is driven vertically a short distance into the granular solid matter and turns then upwards bringing along grains that rise into a crater around a hole formed in the granular solid matter. The obtained crater does not remain high, however, when a new hole is being bored from below into the granular solid matter, but the grains run back into the bored hole providing the desired rolling, i.e. the rolling space. Naturally, the direction in which the flow is directed into the granular solid matter may vary freely, in other words, the direction may be other than what is described above.
[0021] In connection with the above applications, it is also possible to use various screens, if so needed, to limit the grains being carried away from the rolling space 8 into the liquid circulation.
[0022] In the above, the invention is described by means of the application example of Figures 1 and 2. The invention is not limited in any way to said example, however, but it is obvious that other solutions are also possible. Figure 1 shows a cylindrical container, for instance. It is obvious that the container may be different from the cylindrical container shown in the figures, etc.
[0023] The invention may be freely modified within the scope of the claims.

Claims

Claims
1. The invention relates to a method for finely feeding granular solids into a liquid, in which method granular solids (3) and a liquid are fed into a mixing space (2) and mixed together, and a mixture of small solid particles and liquid is discharged from the mixing space (2), characterized in that the granular solid matter (3) in the mixing space is subjected to a liquid flow in such a manner that the liquid flow is driven into a mass consisting of the granular solids (3) and the granular solids are brought to roll controllably in a controlled rolling space (8) locating in the mixing space (2), whereby the grains of the granular solids abrase one another while rolling and tiny particles detaching in abrasion are carried away from the mixing space (2) along with the liquid and large grain particles continue rolling in the controlled rolling space (8).
2. The method of claim 1, characterized in that the liquid flow is directed horizontally into the granular solid matter in the mixing space (2).
3. The method of claim 1, characterized in that the liquid flow is directed vertically into the granular solid matter in the mixing space (2).
4. The method of claim 3, characterized in that the liquid flow is directed into the granular solid matter from above downward, close to the surface of the granular solid matter.
5. The method of any one of claims 1 to 4, c h a r a c t e r i z e d in that the liquid flow into the granular solid matter is directed in such a way that the flow rises in the granular solid matter from below upward, whereby the liquid flow lifts grains of the granular solids therewith upwardly and gravity makes the grains sink, respectively.
6. The method of any one of the preceding claims 1 to 5, characterized in that the rolling space (8) is arranged at a distance from the structures delimiting the mixing space (2).
PCT/FI2013/050469 2012-04-27 2013-04-25 Method for finely feeding granular solids into liquid WO2013160562A1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
US14/395,340 US10010836B2 (en) 2012-04-27 2013-04-25 Method for finely feeding granular solids into liquid
EP13782117.9A EP2841189A4 (en) 2012-04-27 2013-04-25 Method for finely feeding granular solids into liquid

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FI20125469A FI125394B (en) 2012-04-27 2012-04-27 Process for feeding granular suspended matter in liquid
FI20125469 2012-04-27

Publications (1)

Publication Number Publication Date
WO2013160562A1 true WO2013160562A1 (en) 2013-10-31

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US (1) US10010836B2 (en)
EP (1) EP2841189A4 (en)
FI (1) FI125394B (en)
WO (1) WO2013160562A1 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FI125394B (en) * 2012-04-27 2015-09-30 S T Ritvanen Oy Process for feeding granular suspended matter in liquid

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DE1174744B (en) 1960-02-25 1964-07-30 August Klueber Appbau Device for the dosed dissolution of slowly soluble chemicals
US3727760A (en) 1971-02-12 1973-04-17 World Water Resources Inc Water decomposition apparatus
US4345841A (en) * 1980-06-20 1982-08-24 Geosource Inc. Multi-stage centrifugal mixer
JPH0463121A (en) * 1990-07-03 1992-02-28 Sumitomo Jukikai Envirotec Kk Vessel for mixing powder with water
EP0768113A1 (en) 1995-10-11 1997-04-16 Dyckerhoff Aktiengesellschaft Process and device for manufacturing fine cement/ultrafine binder suspensions
WO1997046307A1 (en) * 1996-05-31 1997-12-11 Kevin Johan Fuchsbichler A mixing or dissolving apparatus
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JP2004338121A (en) 2003-05-13 2004-12-02 Shimizu Corp Apparatus and system for manufacturing powdery and granular material mixed liquid
WO2009048337A1 (en) 2007-10-12 2009-04-16 National Oilwell Norway As Means and method for mixing a particulate material and a liquid

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US2590541A (en) 1947-11-14 1952-03-25 Oakite Prod Inc Dissolving apparatus
DE1174744B (en) 1960-02-25 1964-07-30 August Klueber Appbau Device for the dosed dissolution of slowly soluble chemicals
US3727760A (en) 1971-02-12 1973-04-17 World Water Resources Inc Water decomposition apparatus
US4345841A (en) * 1980-06-20 1982-08-24 Geosource Inc. Multi-stage centrifugal mixer
JPH0463121A (en) * 1990-07-03 1992-02-28 Sumitomo Jukikai Envirotec Kk Vessel for mixing powder with water
EP0768113A1 (en) 1995-10-11 1997-04-16 Dyckerhoff Aktiengesellschaft Process and device for manufacturing fine cement/ultrafine binder suspensions
WO1997046307A1 (en) * 1996-05-31 1997-12-11 Kevin Johan Fuchsbichler A mixing or dissolving apparatus
EP1144101B9 (en) * 1998-12-17 2004-03-03 F & P Sortiertechnik GmbH Method, device and installation for continuously treating water
JP2004338121A (en) 2003-05-13 2004-12-02 Shimizu Corp Apparatus and system for manufacturing powdery and granular material mixed liquid
WO2009048337A1 (en) 2007-10-12 2009-04-16 National Oilwell Norway As Means and method for mixing a particulate material and a liquid

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See also references of EP2841189A4

Also Published As

Publication number Publication date
US20150133035A1 (en) 2015-05-14
EP2841189A1 (en) 2015-03-04
FI20125469A (en) 2013-10-28
FI125394B (en) 2015-09-30
US10010836B2 (en) 2018-07-03
EP2841189A4 (en) 2015-12-16

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